JP6398325B2 - Water heater - Google Patents
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- JP6398325B2 JP6398325B2 JP2014108508A JP2014108508A JP6398325B2 JP 6398325 B2 JP6398325 B2 JP 6398325B2 JP 2014108508 A JP2014108508 A JP 2014108508A JP 2014108508 A JP2014108508 A JP 2014108508A JP 6398325 B2 JP6398325 B2 JP 6398325B2
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- heat exchanger
- combustion
- hot water
- temperature
- water supply
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 97
- 238000002485 combustion reaction Methods 0.000 claims description 83
- 238000001514 detection method Methods 0.000 claims description 32
- 239000000567 combustion gas Substances 0.000 claims description 17
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 description 9
- 239000002737 fuel gas Substances 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 238000011144 upstream manufacturing Methods 0.000 description 5
- 230000002159 abnormal effect Effects 0.000 description 4
- 230000005856 abnormality Effects 0.000 description 4
- 238000009835 boiling Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000002390 adhesive tape Substances 0.000 description 1
- 238000005219 brazing Methods 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/20—Arrangement or mounting of control or safety devices
- F24H9/2007—Arrangement or mounting of control or safety devices for water heaters
- F24H9/2035—Arrangement or mounting of control or safety devices for water heaters using fluid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D19/00—Details
- F24D19/0092—Devices for preventing or removing corrosion, slime or scale
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H15/00—Control of fluid heaters
- F24H15/20—Control of fluid heaters characterised by control inputs
- F24H15/288—Accumulation of deposits, e.g. lime or scale
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H15/00—Control of fluid heaters
- F24H15/30—Control of fluid heaters characterised by control outputs; characterised by the components to be controlled
- F24H15/345—Control of fans, e.g. on-off control
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H15/00—Control of fluid heaters
- F24H15/30—Control of fluid heaters characterised by control outputs; characterised by the components to be controlled
- F24H15/355—Control of heat-generating means in heaters
- F24H15/36—Control of heat-generating means in heaters of burners
- F24H15/365—Control of heat-generating means in heaters of burners of two or more burners, e.g. an array of burners
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/20—Arrangement or mounting of control or safety devices
- F24H9/25—Arrangement or mounting of control or safety devices of remote control devices or control-panels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/10—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium
- F24H1/12—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium
- F24H1/14—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form
- F24H1/145—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form using fluid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H15/00—Control of fluid heaters
- F24H15/10—Control of fluid heaters characterised by the purpose of the control
- F24H15/174—Supplying heated water with desired temperature or desired range of temperature
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H15/00—Control of fluid heaters
- F24H15/30—Control of fluid heaters characterised by control outputs; characterised by the components to be controlled
- F24H15/395—Information to users, e.g. alarms
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/0005—Details for water heaters
- F24H9/0042—Cleaning arrangements
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
- Control Of Combustion (AREA)
Description
本発明は給湯装置に関し、特に熱交換器の伝熱管内にスケールが堆積して発生するスケール詰まりを判定する機能を備えた給湯装置に関する。 The present invention relates to a hot water supply apparatus, and more particularly to a hot water supply apparatus having a function of determining scale clogging caused by scale accumulation in a heat transfer tube of a heat exchanger.
従来から、ガス給湯装置、電気給湯装置、石油給湯装置等の熱源に応じた種々の給湯装置が広く一般家庭に普及している。特に、ガス給湯装置は、燃焼用空気を外部から取り込む送風ファン、燃焼用空気と燃料ガスとを混合して燃焼するバーナーユニット、高温の燃焼ガスと伝熱管を流れる水との間で熱交換して水を加熱する熱交換器、熱交換後の排気を外部に排出する為の排気筒等を備えている。 Conventionally, various hot water supply apparatuses according to heat sources such as a gas hot water supply apparatus, an electric hot water supply apparatus, and an oil hot water supply apparatus have been widely used in general households. In particular, a gas hot water supply device exchanges heat between a blower fan that takes in combustion air from the outside, a burner unit that mixes and burns combustion air and fuel gas, and high-temperature combustion gas and water flowing through a heat transfer tube. A heat exchanger for heating the water, an exhaust pipe for discharging the exhaust gas after the heat exchange to the outside.
上記の熱交換器としては、一般的に、伝熱管と、この伝熱管に伝熱可能に固定された複数のフィンからなるフィンアンドチューブ型熱交換器が適用され、伝熱管やフィンをステンレス材料で構成したもの、伝熱管やフィンを銅材料で構成したものが広く採用されている。 As the heat exchanger, generally, a heat transfer tube and a fin-and-tube heat exchanger composed of a plurality of fins fixed to the heat transfer tube so as to be able to transfer heat are applied. In general, the heat transfer tubes and fins made of copper material are widely used.
ところで、上記の熱交換器に供給する上水に対して硬度の高い水道水を使用する場合、水道水に含有されているカルシウムやマグネシウム等と、炭酸イオンや硫酸イオン等とが結合することでスケールが形成され、このスケールが熱交換器の伝熱管内に堆積してしまうことでスケール詰まりが発生し、熱交換器における熱交換効率が悪化するという問題がある。また、給湯装置を長期間使用すると、熱交換器のフィンに煤が付着することで、フィン詰まりが発生し、熱交換器における熱交換効率が悪化するという問題もある。 By the way, when using tap water with high hardness with respect to the tap water supplied to the heat exchanger, calcium ions, magnesium, etc. contained in the tap water are combined with carbonate ions, sulfate ions, etc. A scale is formed, and this scale accumulates in the heat transfer tube of the heat exchanger, causing clogging of the scale, resulting in a problem that heat exchange efficiency in the heat exchanger is deteriorated. Moreover, when a hot-water supply apparatus is used for a long time, a sticking will adhere to the fin of a heat exchanger, a fin clogging will generate | occur | produce and there also exists a problem that the heat exchange efficiency in a heat exchanger deteriorates.
上記のスケール詰まりやフィン詰まりが発生した状態で給湯装置の使用を継続すると、熱交換器が損傷する虞があるので、スケール詰まりやフィン詰まり等の異常が発生した場合には、スケールや煤を除去する為のメンテナンスを行う必要がある。このため、従来から、給湯装置に、スケール詰まり等の異常を検出する機能が備えられている。 Continuing to use the hot water supply device with the above scale clogging or fin clogging may damage the heat exchanger.If an abnormality such as clogging of the scale or clogging of fins occurs, remove the scale or It is necessary to perform maintenance for removal. For this reason, conventionally, the hot water supply apparatus has been provided with a function of detecting an abnormality such as scale clogging.
例えば、特許文献1〜3に記載の装置においては、燃焼停止後の後沸きによる湯水の温度上昇に基づいて、スケール詰まり等を判定する技術が開示されている。また、特許文献4に記載の湯水加熱装置においては、燃焼作動中に熱交換効率が低下したことを検知すると、燃焼量を強制的に減少させ、その後の熱交換効率と基準効率とを比較して、熱交換効率の悪化の原因がスケール詰まりかフィン詰まりかを判定する技術が開示されている。 For example, in the apparatuses described in Patent Documents 1 to 3, a technique for determining scale clogging or the like based on a rise in the temperature of hot water due to post-boiling after stopping combustion is disclosed. Further, in the hot water heater described in Patent Document 4, when it is detected that the heat exchange efficiency has decreased during the combustion operation, the amount of combustion is forcibly reduced, and the subsequent heat exchange efficiency and the reference efficiency are compared. Thus, a technique for determining whether the cause of deterioration in heat exchange efficiency is clogging of scales or clogging of fins is disclosed.
しかし、特許文献1〜3の装置のように、燃焼停止後の後沸きによる湯水の温度上昇に基づいて異常を判定する場合、スケール詰まりによる伝熱不良であるのか、フィン詰まりによる伝熱不良であるのか、熱交換効率の悪化の原因を正確に判定できないため、メンテナンスや対策を行う際に、手間がかかる等の不具合が生じる虞がある。また、燃焼停止直前の燃焼量が低かったり、即湯が実行されていると、異常判定に後沸きによる湯水温度の上昇を利用できないという問題もある。 However, as in the devices of Patent Documents 1 to 3, when an abnormality is determined based on the temperature rise of hot water due to post-boiling after stopping combustion, it is due to heat transfer failure due to scale clogging or heat transfer failure due to fin clogging. The cause of the deterioration of the heat exchange efficiency cannot be accurately determined, and there is a possibility that troubles such as troublesome work may occur when performing maintenance and countermeasures. In addition, if the amount of combustion immediately before the stop of combustion is low, or if instant hot water is being executed, there is a problem that the rise in hot water temperature due to post-boiling cannot be used for abnormality determination.
そこで、特許文献4の湯水加熱装置では、燃焼作動中にスケール詰まりかフィン詰まりかの原因を特定する判定が行われているが、この特許文献4の技術では、燃焼作動中に原因の特定を行う為に、通常の給湯運転状態であっても強制的に燃焼量を減少させるので、使用者が意図せずに、給湯量や給湯温度が変動してしまうという問題が生じる。 Therefore, in the hot water heater of Patent Document 4, determination is made to identify the cause of scale clogging or fin clogging during the combustion operation. However, in the technique of Patent Document 4, the cause is identified during the combustion operation. Therefore, since the amount of combustion is forcibly reduced even in a normal hot water supply operation state, there arises a problem that the amount of hot water supply and the hot water supply temperature fluctuate unintentionally by the user.
本発明の目的は、給湯装置において、簡単な方法によってスケール詰まりを確実に判定可能なもの、等を提供することである。 An object of the present invention is to provide a hot water supply apparatus that can reliably determine scale clogging by a simple method.
請求項1の給湯装置は、燃焼ガスによって上水を加熱する為のフィンアンドチューブ型熱交換器と、この熱交換器を収納する為の熱交換器缶体とを備えた給湯装置において、前記熱交換器缶体の表面温度を検知する為の温度検知手段と、この温度検知手段によって検知される検知温度が設定温度以上になった場合に前記熱交換器の伝熱管内にスケールが堆積していると判定する判定手段とを備え、前記温度検知手段は、給湯運転時には常時燃焼する燃焼部の直上であって前記熱交換器の前記燃焼部に最も近い伝熱管の下流側の近傍において前記熱交換器缶体の表面に設けられたことを特徴としている。 The hot water supply apparatus according to claim 1 is a hot water supply apparatus including a fin-and-tube heat exchanger for heating clean water with combustion gas and a heat exchanger can body for housing the heat exchanger. A temperature detector for detecting the surface temperature of the heat exchanger can body, and a scale is deposited in the heat transfer tube of the heat exchanger when the detected temperature detected by the temperature detector exceeds a set temperature. The temperature detection means is located immediately above the combustion section that always burns during hot water supply operation and in the vicinity of the downstream side of the heat transfer tube closest to the combustion section of the heat exchanger. It is provided on the surface of the heat exchanger can body .
請求項1の発明によれば、給湯装置は、熱交換器缶体の表面温度を検知する為の温度検知手段と、この温度検知手段によって検知される検知温度が設定温度以上になった場合に熱交換器の伝熱管内にスケールが堆積していると判定する判定手段とを備えたので、熱交換器缶体の表面温度が設定温度以上になった場合、熱交換器にスケール詰まりが発生したと把握することができる。 According to the first aspect of the present invention, the hot water supply apparatus includes a temperature detecting means for detecting the surface temperature of the heat exchanger can body, and a case where the detected temperature detected by the temperature detecting means is equal to or higher than the set temperature. Judgment means that determines that scale has accumulated in the heat exchanger tubes of the heat exchanger, so if the surface temperature of the heat exchanger can exceeds the set temperature, scale clogging occurs in the heat exchanger Can be grasped.
フィン詰まりの場合、燃焼ガスが熱交換器のフィン間を流れ難くなり、熱交換器に回収される燃焼ガスの熱量が低下し、燃焼ガスが高い温度を維持したまま排気されるので、熱交換器の温度が上昇せず、熱交換器缶体の表面温度も上昇しない。これに対し、スケール詰まりの場合、燃焼ガスによって熱交換器の温度は上昇するが、熱交換器の伝熱管に流れる水へ効率良く伝熱できないので、熱交換器自体の温度が異常に上昇し、それに伴い熱交換器缶体の表面温度も異常に上昇する。 In the case of clogged fins, it becomes difficult for the combustion gas to flow between the fins of the heat exchanger, the amount of combustion gas recovered in the heat exchanger decreases, and the combustion gas is exhausted while maintaining a high temperature. The temperature of the vessel does not rise, and the surface temperature of the heat exchanger can body does not rise. On the other hand, in the case of scale clogging, the temperature of the heat exchanger rises due to the combustion gas, but since the heat cannot be transferred efficiently to the water flowing through the heat exchanger tubes, the temperature of the heat exchanger itself rises abnormally. As a result, the surface temperature of the heat exchanger can body also rises abnormally.
即ち、温度検知手段によって熱交換器缶体の表面温度を直接測定し、スケール詰まりにより熱交換器の伝熱が阻害されて発生する熱交換器缶体の異常な温度上昇を検知することで、スケール詰まりかフィン詰まりかを区別して判定することができるので、燃焼停止後の湯水温度の上昇や燃焼作動中の熱交換効率の変化で判定する方法と比較して、燃焼運転中であってもスケール詰まりを正確に判定することができる。また、スケール詰まりを判定する際に、使用者の意図に反して給湯量や給湯温度が変動するのを防止することができる。 That is, by directly measuring the surface temperature of the heat exchanger can body by the temperature detection means, and detecting an abnormal temperature rise of the heat exchanger can body that occurs due to the heat transfer of the heat exchanger being hindered by scale clogging, Since it is possible to distinguish between scale clogging and fin clogging, compared to the method of judging by the rise in hot water temperature after stopping combustion or change in heat exchange efficiency during combustion operation, even during combustion operation Scale clogging can be accurately determined. Moreover, when determining scale clogging, it is possible to prevent fluctuations in the amount of hot water supply and the temperature of hot water supply against the intention of the user.
そして、温度検知手段は、給湯運転時には常時燃焼する燃焼部の直上であって熱交換器の燃焼部に最も近い伝熱管の下流側の近傍において熱交換器缶体の表面に設けられたので、伝熱管のスケール詰まりが発生する可能性が高い箇所の近傍に設けられた温度検知手段によって、熱交換器缶体の異常な温度上昇を検知することで、スケール詰まりを確実に且つ迅速に把握することができる。 And since the temperature detection means is provided on the surface of the heat exchanger can body in the vicinity of the downstream side of the heat transfer tube closest to the combustion portion of the heat exchanger, immediately above the combustion portion that always burns during hot water supply operation, By detecting the abnormal temperature rise of the heat exchanger can body by the temperature detection means provided near the place where the possibility of scale clogging of the heat transfer tube is high, the scale clogging can be grasped reliably and quickly. be able to.
また、熱交換器缶体の上述したような箇所に温度検知手段を設け、熱交換器缶体の表面温度を利用してスケール詰まりを判定するので、燃焼作動中にもスケール詰まりの判定を容易に実行することができ、バーナーユニットの最低燃焼量による燃焼作動に対応可能であり、即湯に対応可能であり、大能力の給湯装置にも対応可能である。 In addition, temperature detection means is provided at the above-mentioned locations of the heat exchanger can body, and scale clogging is determined using the surface temperature of the heat exchanger can body, so it is easy to determine scale clogging even during combustion operation. It can be applied to the combustion operation with the minimum combustion amount of the burner unit, can be applied to instant hot water, and can be applied to a large capacity hot water supply device.
以下、本発明を実施するための形態について実施例に基づいて説明する。 Hereinafter, modes for carrying out the present invention will be described based on examples.
先ずは、本発明の給湯装置1の全体構成について説明する。
図1〜図4に示すように、給湯装置1は、給湯機器や暖房機器等の熱源機として適用されるものであり、燃料ガスを燃焼して燃焼ガスに含まれる熱を利用して水又は湯水の加熱を行うガス給湯器を構成している。
First, the whole structure of the hot water supply device 1 of the present invention will be described.
As shown in FIGS. 1 to 4, the hot water supply device 1 is applied as a heat source device such as a hot water supply device or a heating device, and burns fuel gas to use water contained in the combustion gas or water. It constitutes a gas water heater that heats hot water.
即ち、給湯装置1は、燃焼用空気を供給する為の送風ファン2、燃料ガスを燃焼させるバーナー部3、このバーナー部3による燃焼ガスと水との間で熱交換する熱交換器部4、この熱交換器部4による熱交換後の排気を排出する排気筒5、入水管6aと出湯管6b等の各種配管類や各種機器を駆動制御する制御ユニット7等を備えている。 That is, the hot water supply device 1 includes a blower fan 2 for supplying combustion air, a burner unit 3 for burning fuel gas, a heat exchanger unit 4 for exchanging heat between the combustion gas and water by the burner unit 3, An exhaust pipe 5 for discharging the exhaust gas after heat exchange by the heat exchanger section 4, various pipes such as a water inlet pipe 6a and a hot water outlet pipe 6b, and a control unit 7 for driving and controlling various devices are provided.
バーナー部3は、燃料供給管(図示略)から供給される燃料ガスと送風ファン2から供給される燃焼用空気とを混合して燃焼するバーナーユニット11と、このバーナーユニット11を収容したバーナー缶体12と、このバーナー缶体12内におけるバーナーユニット11の上方の燃焼空間13等を備えている。バーナー缶体12は、上方が開口された直方体形状に構成されている。バーナー缶体12の下端部には、送風ファン2が設けられている。 The burner unit 3 includes a burner unit 11 that mixes and burns fuel gas supplied from a fuel supply pipe (not shown) and combustion air supplied from the blower fan 2, and a burner can containing the burner unit 11. A body 12 and a combustion space 13 above the burner unit 11 in the burner can body 12 are provided. The burner can body 12 is configured in a rectangular parallelepiped shape having an upper opening. A blower fan 2 is provided at the lower end of the burner can body 12.
バーナーユニット11は、左右方向に平行に配置された10本の燃焼管14を備え、複数段の(例えば3段)の燃焼段11a〜11cからなる多段式に構成されている(図1,図2,図4参照)。各燃焼段11a〜11cは、例えば5本、2本、3本の燃焼管14を夫々備え、対応する燃料供給管に夫々接続されている。各燃焼段11a〜11cは、制御ユニット7によって単独で燃焼制御可能であり、各種の運転に応じて燃焼作動される燃焼段11a〜11cの段数及びその出力が調整される。 The burner unit 11 includes ten combustion pipes 14 arranged in parallel in the left-right direction, and is configured in a multistage system including a plurality of (for example, three) combustion stages 11a to 11c (FIGS. 1 and 1). 2, see FIG. Each of the combustion stages 11a to 11c includes, for example, five, two, and three combustion pipes 14, respectively, and is connected to a corresponding fuel supply pipe. Each of the combustion stages 11a to 11c can be independently controlled by the control unit 7, and the number of stages of the combustion stages 11a to 11c and the output thereof are adjusted according to various operations.
給湯運転時には、例えば、中央の燃焼段11bの2本の燃焼管14のみを燃焼する1段燃焼段階、中央と右側の燃焼段11b,11cの5本の燃焼管14を燃焼する2段燃焼段階、左側と中央の燃焼段11a,11bの7本の燃焼管14を燃焼する3段燃焼段階、全ての燃焼段11a〜11cの10本の燃焼管14を燃焼する4段燃焼段階の4段階に燃焼段階を切り換えて燃焼作動する。尚、中央の燃焼段11bは、給湯運転時には常時燃焼される燃焼部に相当する。 During the hot water supply operation, for example, a one-stage combustion stage in which only the two combustion tubes 14 in the central combustion stage 11b are combusted, and a two-stage combustion stage in which the five combustion tubes 14 in the center and right combustion stages 11b and 11c are combusted. The four-stage combustion stage includes the three-stage combustion stage for burning the seven combustion tubes 14 of the left and center combustion stages 11a and 11b, and the four-stage combustion stage for burning the ten combustion pipes 14 of all the combustion stages 11a to 11c. The combustion operation is performed by switching the combustion stage. The central combustion stage 11b corresponds to a combustion section that is always combusted during a hot water supply operation.
図2,図3に示すように、バーナーユニット11の燃焼段11bの上方の燃焼空間13には、イグナイター15とフレームロッド16とが夫々配置されている。イグナイター15とフレームロッド16は、バーナー缶体12の前側板12a左右方向の中央部の右寄り部分(燃焼段11bに対応する部分)に夫々取り付けられている。フレームロッド16は、イグナイター15の右側に隣接状に取り付けられている。 As shown in FIGS. 2 and 3, an igniter 15 and a frame rod 16 are respectively arranged in the combustion space 13 above the combustion stage 11 b of the burner unit 11. The igniter 15 and the frame rod 16 are respectively attached to the right side portion (portion corresponding to the combustion stage 11b) of the center portion of the front side plate 12a of the burner can body 12 in the left-right direction. The frame rod 16 is attached adjacent to the right side of the igniter 15.
イグナイター15は、バーナーユニット11に設けられた点火ターゲットとの間で点火スパークを生じさせることで、バーナーユニット11から噴出される燃料空気混合気に火炎を生じさせる為のものであり、燃焼空間13に突き出すように且つ斜め下方に向かって延びるように取り付けられている。 The igniter 15 generates an ignition spark with an ignition target provided in the burner unit 11, thereby generating a flame in the fuel-air mixture ejected from the burner unit 11. It is attached so that it may protrude to diagonally downward.
フレームロッド16は、バーナーユニット11に生じた火炎の間に交流電圧を印加し、火炎のイオン化による導電性や整流作用を利用して、フレームロッド16から火炎へ流れる直流電流を検知することで、火炎の有無を検出する為のものであり、燃焼空間13に突き出すように且つ真っ直ぐ延びるように取り付けられている。 The flame rod 16 applies an alternating voltage between the flames generated in the burner unit 11, and detects the direct current flowing from the flame rod 16 to the flame by using the conductivity and rectification action due to the ionization of the flame. It is for detecting the presence or absence of a flame, and is attached so as to protrude into the combustion space 13 and extend straight.
図1〜図4に示すように、熱交換器部4は、燃焼ガスの熱を回収する熱交換器21と、この熱交換器21を収容する熱交換器缶体22等を備えている。熱交換器缶体22の上端部に、前方に開口した排気口5aを有する排気筒5が設けられている。熱交換器缶体22は、平面視矩形枠状に構成されている。熱交換器缶体22の下端部とバーナー缶体12の上端部とは、カシメやビス締結により接合されている。熱交換器缶体22の周囲には、温度ヒューズ23が設けられている(図2,図3参照)。 As shown in FIGS. 1 to 4, the heat exchanger section 4 includes a heat exchanger 21 that recovers the heat of the combustion gas, a heat exchanger can body 22 that accommodates the heat exchanger 21, and the like. An exhaust tube 5 having an exhaust port 5a opened forward is provided at the upper end of the heat exchanger can body 22. The heat exchanger can body 22 is configured in a rectangular frame shape in plan view. The lower end portion of the heat exchanger can body 22 and the upper end portion of the burner can body 12 are joined by caulking or screw fastening. A thermal fuse 23 is provided around the heat exchanger can body 22 (see FIGS. 2 and 3).
熱交換器21は、伝熱管25と、この伝熱管25に伝熱可能に固定された複数のフィン26等からなるフィンアンドチューブ型熱交換器を構成している。伝熱管25及びフィン26は、銅製のものであるが、特にこの材質に限定する必要はなく、ステンレス製のものであっても良い。 The heat exchanger 21 constitutes a fin-and-tube heat exchanger including a heat transfer tube 25 and a plurality of fins 26 and the like fixed to the heat transfer tube 25 so as to transfer heat. The heat transfer tubes 25 and the fins 26 are made of copper, but are not particularly limited to this material, and may be made of stainless steel.
図1,図3に示すように、熱交換器缶体22の内部において、熱交換器21は、排気筒5の下端に連なる上段側(燃焼ガス流の下流側)の上段熱交換領域21Aと、燃焼空間13の上端に連なる下段側(燃焼ガス流の上流側)の下段熱交換領域21Bとを備えた2段構造である。 As shown in FIGS. 1 and 3, in the heat exchanger can body 22, the heat exchanger 21 includes an upper heat exchange region 21 </ b> A connected to the lower end of the exhaust pipe 5 (downstream side of the combustion gas flow) and the upper heat exchange region 21 </ b> A. , A two-stage structure including a lower heat exchange region 21B connected to the upper end of the combustion space 13 (the upstream side of the combustion gas flow).
伝熱管25は、2段に亙って平行状に配置された複数の直管部27と、この複数の直管部27の端部同士を連結する複数の連結管部28とを備えている。上段熱交換領域21Aには、4本の直管部27が配設され、下段熱交換領域21Bには、4本の直管部27が配設され、上段熱交換領域21A及び下段熱交換領域21Bの夫々において、伝熱管25は、平面視蛇行形状に夫々構成されている(図4参照)。 The heat transfer tube 25 includes a plurality of straight tube portions 27 arranged in parallel over two stages, and a plurality of connection tube portions 28 that connect ends of the plurality of straight tube portions 27. . Four straight pipe portions 27 are arranged in the upper heat exchange area 21A, and four straight pipe portions 27 are arranged in the lower heat exchange area 21B, and the upper heat exchange area 21A and the lower heat exchange area In each of 21B, the heat exchanger tubes 25 are each configured in a meandering shape in plan view (see FIG. 4).
入水管6aの下流側端部が、下段熱交換領域21Bの上流側(後側)の直管部27aに接続され、下段熱交換領域21Bの下流側(前側)の直管部27bが、上段熱交換領域21Aの上流側(前側)の直管部27cに連結管部28を介して接続され、上段熱交換領域21Aの下流側(後側)の直管部27dが、出湯管6bの上流側端部に接続されている。 The downstream end of the inlet pipe 6a is connected to the upstream (rear) straight pipe portion 27a of the lower heat exchange area 21B, and the downstream (front) straight pipe section 27b of the lower heat exchange area 21B is connected to the upper stage. The straight pipe portion 27c on the upstream side (front side) of the heat exchange region 21A is connected via the connecting pipe portion 28, and the straight pipe portion 27d on the downstream side (rear side) of the upper heat exchange region 21A is located upstream of the outlet pipe 6b. Connected to the side edge.
給湯装置1において、バーナーユニット11に燃料供給管から燃料ガスが供給されると共に送風ファン2から燃焼用空気が供給され、燃料ガスと空気とが混合された燃料空気混合気が燃焼されて燃焼空間13に火炎が形成され、この火炎の燃焼熱(燃焼ガス)は、燃焼空間13を通って熱交換器21内の水を加熱し、その後、排気は排気筒5を介して排気口5aから外部に排出される。 In the hot water supply apparatus 1, the fuel gas is supplied to the burner unit 11 from the fuel supply pipe and the combustion air is supplied from the blower fan 2, and the fuel-air mixture in which the fuel gas and the air are mixed is burned to burn the combustion space. A flame is formed in 13, and the combustion heat (combustion gas) of this flame heats the water in the heat exchanger 21 through the combustion space 13, and then the exhaust is discharged from the exhaust port 5 a through the exhaust tube 5 to the outside. To be discharged.
一方、熱交換器21においては、外部の上水源から入水管6aに上水が供給されると、この上水は、先ずは、熱交換器21の下段熱交換領域21Bの伝熱管25を流れ、次に、熱交換器21の上段熱交換領域21Aの伝熱管25を流れ、上述のように熱交換器21にて上水は加熱されて湯水となり、出湯管6bから外部に出湯される。 On the other hand, in the heat exchanger 21, when clean water is supplied from an external clean water source to the water intake pipe 6a, the clean water first flows through the heat transfer pipe 25 in the lower heat exchange region 21B of the heat exchanger 21. Next, it flows through the heat transfer pipe 25 in the upper heat exchange region 21A of the heat exchanger 21, and the hot water is heated in the heat exchanger 21 as described above to become hot water, and discharged from the hot water discharge pipe 6b to the outside.
次に、本発明に関連する温度検知センサ31について説明する。
図2,図3に示すように、給湯装置1は、熱交換器缶体22の表面温度を検知する為の温度検知センサ31(温度検知手段に相当する)を備えている。温度検知センサ31は、給湯運転時には常時燃焼する燃焼段11b(燃焼部)の直上であって、熱交換器21の燃焼段11bに最も近い下段熱交換領域21Bの伝熱管25の下流側の近傍において熱交換器缶体22の表面に設けられている。
Next, the temperature detection sensor 31 related to the present invention will be described.
As shown in FIGS. 2 and 3, the hot water supply device 1 includes a temperature detection sensor 31 (corresponding to temperature detection means) for detecting the surface temperature of the heat exchanger can body 22. The temperature detection sensor 31 is directly above the combustion stage 11b (combustion part) that always burns during the hot water supply operation, and in the vicinity of the downstream side of the heat transfer tube 25 in the lower heat exchange region 21B closest to the combustion stage 11b of the heat exchanger 21. Are provided on the surface of the heat exchanger can body 22.
即ち、温度検知センサ31は、下段熱交換領域21Bの下流側の直管部27bにおける燃焼段11bの直上の通路部32の近傍であって(図4参照)、バーナー缶体12の前側板12aのフレームロッド16取り付け部分の直上に位置する熱交換器缶体22の前側板22aの表面に設けられている(図2,図3参照)。 That is, the temperature detection sensor 31 is in the vicinity of the passage portion 32 immediately above the combustion stage 11b in the straight pipe portion 27b on the downstream side of the lower heat exchange region 21B (see FIG. 4), and the front plate 12a of the burner can body 12 Is provided on the surface of the front side plate 22a of the heat exchanger can body 22 located immediately above the mounting portion of the frame rod 16 (see FIGS. 2 and 3).
温度検知センサ31は、熱電対31aと、この熱電対31aから延びる1対のリード線31b等から構成された公知の温度検知センサで構成され、ロウ付け又は接着テープによって固定されている。1対のリード線31bは制御ユニット7に接続され、温度検知センサ31の熱交換器缶体22の前側板12aの表面温度に基づく検知信号が制御ユニット7に供給される。 The temperature detection sensor 31 is composed of a known temperature detection sensor including a thermocouple 31a and a pair of lead wires 31b extending from the thermocouple 31a, and is fixed by brazing or adhesive tape. The pair of lead wires 31 b is connected to the control unit 7, and a detection signal based on the surface temperature of the front plate 12 a of the heat exchanger can body 22 of the temperature detection sensor 31 is supplied to the control unit 7.
次に、制御ユニット7について説明する。
図1,図2に示すように、制御ユニット7は、給湯装置1の制御を行うものであり、各種のセンサが電気的に接続され、各種のセンサからの検知信号を受信するように構成されている。制御ユニット7は、操作リモコン等によって設定された給湯温度、給湯栓に供給される給湯量、各種のセンサから受信した検知信号に基づき、送風ファン2やバーナーユニット11等を駆動制御し、給湯運転を実行する。
Next, the control unit 7 will be described.
As shown in FIGS. 1 and 2, the control unit 7 controls the hot water supply device 1 and is configured such that various sensors are electrically connected and receive detection signals from the various sensors. ing. The control unit 7 controls driving of the blower fan 2, the burner unit 11 and the like based on the hot water temperature set by the operation remote controller, the amount of hot water supplied to the hot water tap, and detection signals received from various sensors, and hot water supply operation Execute.
次に、本発明に関連するスケール詰まり判定運転制御について説明する。
制御ユニット7(判定手段に相当する)は、温度検知センサ31によって検知される検知温度(熱交換器缶体22の表面温度)が設定温度以上になった場合に熱交換器21の伝熱管25内にスケールが堆積していると判定するスケール詰まり判定運転制御を実行可能である。
Next, the scale clogging determination operation control related to the present invention will be described.
The control unit 7 (corresponding to the determination means) is configured so that the heat transfer tube 25 of the heat exchanger 21 is detected when the detected temperature (surface temperature of the heat exchanger can body 22) detected by the temperature detecting sensor 31 is equal to or higher than the set temperature. It is possible to execute scale clogging determination operation control that determines that scale is accumulated in the inside.
次に、この給湯装置1の給湯運転中に、制御ユニット7により自動的に実行されるスケール詰まり判定運転制御について、図5のフローチャートに基づいて説明する。尚、図中の符号Si(i=1,2,・・)は各ステップを示す。このスケール詰まり判定運転制御の制御プログラムは、制御ユニット7に予め格納されている。 Next, scale clogging determination operation control automatically executed by the control unit 7 during the hot water supply operation of the hot water supply device 1 will be described based on the flowchart of FIG. In the figure, the symbol Si (i = 1, 2,...) Indicates each step. A control program for the scale clogging determination operation control is stored in the control unit 7 in advance.
図5のフローチャートにおいて、この制御が開始されると、最初にS1において、制御ユニット7は、給湯装置1が給湯運転中か否かを判定する。即ち、給湯装置1が給湯運転中の場合、つまり、制御ユニット7が給湯運転に基づく信号を受信している場合、S1の判定がYesとなり、S2に移行し、S1の判定がNoのうちはS1を繰り返す。 In the flowchart of FIG. 5, when this control is started, first, in S <b> 1, the control unit 7 determines whether or not the hot water supply device 1 is in a hot water supply operation. That is, when the hot water supply apparatus 1 is in the hot water supply operation, that is, when the control unit 7 receives a signal based on the hot water supply operation, the determination of S1 is Yes, the process proceeds to S2, and the determination of S1 is No. Repeat S1.
次に、S2において、制御ユニット7は、温度検知センサ31の検知信号を読み込み、この検知信号に基づいて、熱交換器缶体22の前側板22aの表面温度を算出し、S3に移行する。 Next, in S2, the control unit 7 reads the detection signal of the temperature detection sensor 31, calculates the surface temperature of the front side plate 22a of the heat exchanger can body 22 based on this detection signal, and proceeds to S3.
次に、S3において、熱交換器缶体22の表面温度が設定温度(例えば180〜200度程度)を超えているか否かの判定を行い、表面温度が設定温度を超えている場合、S3の判定がYesとなり、S4に移行する。表面温度が設定温度以下の場合、S3の判定がNoとなり、熱交換器21が正常であると判定して、リターンする。尚、設定温度は、上記の温度に限定する必要はなく、適宜変更可能である。 Next, in S3, it is determined whether or not the surface temperature of the heat exchanger can body 22 exceeds a set temperature (for example, about 180 to 200 degrees). If the surface temperature exceeds the set temperature, The determination is Yes, and the process proceeds to S4. If the surface temperature is equal to or lower than the set temperature, the determination in S3 is No, it is determined that the heat exchanger 21 is normal, and the process returns. The set temperature need not be limited to the above temperature, and can be changed as appropriate.
ここで、給湯運転時には、上述したように、バーナーユニット11を、要求熱量に応じて4段階に燃焼段階を調整して燃焼作動するが、中央の燃焼段11bの2本の燃焼管14は、最低燃焼量で燃焼作動可能であり、給湯運転時には常時燃焼される。 Here, at the time of the hot water supply operation, as described above, the burner unit 11 is operated by adjusting the combustion stage in four stages according to the required heat quantity, but the two combustion pipes 14 in the central combustion stage 11b are Combustion operation is possible with the minimum combustion amount, and combustion is always performed during hot water supply operation.
一方、熱交換器21において、下段熱交換領域21Bにおける複数の直管部27の燃焼段11bの直上に位置する部分は、燃焼段11bの2本の燃焼管14の火炎に常時炙られることになる。また、伝熱管25に供給される上水は、上流側の直管部27aから下流側の直管部27bに向かって蛇行状に流れて加熱されるため、下段熱交換領域21Bにおいては直管部27bの湯水温度が最も上昇する。 On the other hand, in the heat exchanger 21, the portion of the plurality of straight pipe portions 27 located directly above the combustion stage 11b in the lower heat exchange region 21B is constantly burned by the flames of the two combustion pipes 14 of the combustion stage 11b. Become. Moreover, since the clean water supplied to the heat transfer pipe 25 flows in a meandering manner from the upstream straight pipe portion 27a toward the downstream straight pipe portion 27b and is heated, the straight pipe is provided in the lower heat exchange region 21B. The hot water temperature of the part 27b rises most.
このため、常時火炎で炙られる複数の直管部27のうちの直管部27bの通路部32が、給湯運転時には湯水温度が最も高くなる可能性があるので、他の部分と比較してスケールが堆積しやすい。直管部27bの通路部32にスケール詰まりが発生すると、熱交換器21の伝熱不良によって、通路部32の近傍の熱交換器缶体22の表面温度が、180〜200度程度に異常に上昇する。熱交換器21が正常の場合、熱交換器缶体22の表面温度は、通常は120度程度を維持するので、この表面温度を利用することで、スケール詰まりを把握することができる。 For this reason, since the channel | path part 32 of the straight pipe part 27b of the some straight pipe parts 27 always burned with a flame may have the highest hot water temperature at the time of hot water supply operation, it is a scale compared with another part. Is easy to deposit. When scale clogging occurs in the passage portion 32 of the straight pipe portion 27b, the surface temperature of the heat exchanger can body 22 in the vicinity of the passage portion 32 becomes abnormal to about 180 to 200 degrees due to heat transfer failure of the heat exchanger 21. To rise. When the heat exchanger 21 is normal, the surface temperature of the heat exchanger can body 22 is normally maintained at about 120 ° C., so that scale clogging can be grasped by using this surface temperature.
尚、フィン詰まりの場合、燃焼ガスが熱交換器21のフィン26間を流れ難くなり、熱交換器21に回収される燃焼ガスの熱量が低下し、燃焼ガスが高い温度を維持したまま排気されるので、熱交換器21の温度が上昇せず、熱交換器缶体22の表面温度も上昇しない。これに対して、スケール詰まりの場合、燃焼ガスによって熱交換器21の温度は上昇するが、熱交換器21の伝熱管25に流れる水へ効率良く伝熱できないので、熱交換器21自体の温度が異常に上昇し、それに伴い熱交換器缶体22の表面温度も上昇する。 In the case of clogged fins, it becomes difficult for the combustion gas to flow between the fins 26 of the heat exchanger 21, the amount of heat of the combustion gas recovered by the heat exchanger 21 decreases, and the combustion gas is exhausted while maintaining a high temperature. Therefore, the temperature of the heat exchanger 21 does not rise, and the surface temperature of the heat exchanger can body 22 does not rise. On the other hand, in the case of scale clogging, the temperature of the heat exchanger 21 rises due to the combustion gas, but it cannot efficiently transfer heat to the water flowing through the heat transfer tube 25 of the heat exchanger 21, so the temperature of the heat exchanger 21 itself. Rises abnormally, and accordingly, the surface temperature of the heat exchanger can 22 also rises.
次に、S4において、制御ユニット7は、熱交換器21にスケール詰まりが発生していると判定し、スケール詰まりを操作リモコンの表示や音声等を介して使用者に報知して、その後、リターンする。尚、スケール詰まりを報知した後、給湯運転を継続しても良いし、スケール詰まりを報知した直後に、給湯運転を停止しても良いし、スケール詰まりを報知して所定の時間経過後に、給湯運転を停止しても良い。 Next, in S4, the control unit 7 determines that scale clogging has occurred in the heat exchanger 21, notifies the user of scale clogging via the display of the operation remote controller, voice, etc., and then returns. To do. After notifying scale clogging, the hot water supply operation may be continued, or immediately after the scale clogging is notified, the hot water supply operation may be stopped, or the scale clogging is notified and a predetermined time has elapsed. Operation may be stopped.
次に、本発明の給湯装置1の作用及び効果について説明する。
本発明の給湯装置1は、熱交換器缶体22の表面温度を検知する為の温度検知センサ31と、この温度検知センサ31によって検知される検知温度が設定温度以上になった場合に熱交換器21の伝熱管25内にスケールが堆積していると判定する制御ユニット7とを備えたので、熱交換器缶体22の表面温度が設定温度以上になった場合、熱交換器21にスケール詰まりが発生したと把握することができる。
Next, the operation and effect of the hot water supply apparatus 1 of the present invention will be described.
The water heater 1 according to the present invention includes a temperature detection sensor 31 for detecting the surface temperature of the heat exchanger can 22 and heat exchange when the detected temperature detected by the temperature detection sensor 31 is equal to or higher than a set temperature. Since the control unit 7 for determining that the scale is accumulated in the heat transfer tube 25 of the heat exchanger 21 is provided, when the surface temperature of the heat exchanger can body 22 becomes equal to or higher than the set temperature, the heat exchanger 21 has a scale. It can be understood that clogging has occurred.
即ち、温度検知センサ31によって熱交換器缶体22の表面温度を直接測定し、スケール詰まりにより熱交換器21の伝熱が阻害されて発生する熱交換器缶体22の異常な温度上昇を検知することで、スケール詰まりかフィン詰まりかを区別して判定することができるので、燃焼停止後の湯水温度の上昇や燃焼作動中の熱交換効率の変化で判定する方法と比較して、燃焼運転中であってもスケール詰まりを正確に判定することができる。また、スケール詰まりを判定する際に、使用者の意図に反して給湯量や給湯温度が変動するのを防止することができる。 That is, the surface temperature of the heat exchanger can body 22 is directly measured by the temperature detection sensor 31, and an abnormal temperature rise of the heat exchanger can body 22 generated due to the blockage of the heat exchanger 21 due to clogging of the scale is detected. By doing so, it is possible to distinguish between scale clogging and fin clogging, so compared to the method of judging by the rise in hot water temperature after combustion stop and change in heat exchange efficiency during combustion operation, Even so, scale clogging can be accurately determined. Moreover, when determining scale clogging, it is possible to prevent fluctuations in the amount of hot water supply and the temperature of hot water supply against the intention of the user.
また、温度検知センサ31は、給湯運転時には常時燃焼する燃焼部の直上であって熱交換器21の燃焼部に最も近い伝熱管25の下流側の近傍において熱交換器缶体22の表面に設けられたので、伝熱管25のスケール詰まりが発生する可能性が高い箇所の近傍に設けられた温度検知センサ31によって、熱交換器缶体22の異常な温度上昇を検知することで、スケール詰まりを確実に且つ迅速に把握することができる。 Further, the temperature detection sensor 31 is provided on the surface of the heat exchanger can body 22 in the vicinity of the downstream side of the heat transfer tube 25 that is immediately above the combustion portion that always burns during hot water supply operation and closest to the combustion portion of the heat exchanger 21. Therefore, the temperature clogging of the heat exchanger tube 22 is detected by the temperature detection sensor 31 provided in the vicinity of the portion where the possibility of the clogging of the heat transfer tube 25 is likely to occur. It is possible to grasp reliably and quickly.
さらに、熱交換器缶体22の上述したような箇所に温度検知センサ31を設け、熱交換器缶体22の表面温度を利用してスケール詰まりを判定するので、燃焼作動中にもスケール詰まりの判定を容易に実行することができ、バーナーユニット11の最低燃焼量の燃焼作動に対応可能であり、即湯に対応可能であり、大能力の給湯装置にも対応可能である。 Furthermore, since the temperature detection sensor 31 is provided at the above-described portion of the heat exchanger can body 22 and the scale clogging is determined using the surface temperature of the heat exchanger can body 22, the scale clogging is also performed during the combustion operation. The determination can be easily performed, the combustion operation with the minimum combustion amount of the burner unit 11 can be handled, the hot water can be handled, and the hot water supply device with high capacity can also be handled.
次に、前記実施例を部分的に変更した形態について説明する。
[1]前記実施例の温度検知センサ31は、直管部27bの通路部32の近傍における熱交換器缶体22の前側板22aの表面に設けられているが、この位置に限定する必要はなく、伝熱管25内で湯水温度が最も上昇する可能性がある通路部の近傍であれば、適宜変更可能である。
Next, a mode in which the above embodiment is partially changed will be described.
[1] The temperature detection sensor 31 of the above embodiment is provided on the surface of the front plate 22a of the heat exchanger can body 22 in the vicinity of the passage portion 32 of the straight pipe portion 27b, but it is necessary to limit to this position. If it is in the vicinity of the passage where the hot water temperature is likely to rise most in the heat transfer tube 25, it can be changed as appropriate.
[2]前記実施例の温度検知センサ31は、主に熱電対31aで構成されているが、この構造に限定する必要はなく、サーミスタで構成されたものを採用しても良いし、赤外線センサで構成されたものを採用しても良く、適宜変更可能である。 [2] The temperature detection sensor 31 of the above embodiment is mainly composed of a thermocouple 31a. However, the temperature detection sensor 31 is not limited to this structure, and may be composed of a thermistor or an infrared sensor. What was comprised by this may be employ | adopted and it can change suitably.
[3]前記実施例のバーナーユニット11は、10本の燃焼管14を備え、3段の燃焼段11a〜11cからなる多段式に構成されているが、特にこの構造に限定する必要はなく、バーナーユニットの燃焼段の数や各燃焼段の燃焼管の数は、適宜変更可能である。 [3] The burner unit 11 of the above-described embodiment includes ten combustion pipes 14 and is configured in a multistage system including three combustion stages 11a to 11c. However, the present invention is not particularly limited to this structure. The number of combustion stages in the burner unit and the number of combustion tubes in each combustion stage can be changed as appropriate.
[4]その他、当業者であれば、本発明の趣旨を逸脱することなく、前記実施例に種々の変更を付加した形態で実施可能であり、本発明はそのような変更形態を包含するものである。 [4] In addition, those skilled in the art can implement the present invention by adding various modifications without departing from the spirit of the present invention, and the present invention includes such modifications. It is.
1 給湯装置
7 制御ユニット(判定手段)
21 熱交換器
22 熱交換器缶体
25 伝熱管
31 温度検知センサ(温度検知手段)
1 Water heater 7 Control unit (determination means)
21 heat exchanger 22 heat exchanger can body 25 heat transfer tube 31 temperature detection sensor (temperature detection means)
Claims (1)
前記熱交換器缶体の表面温度を検知する為の温度検知手段と、この温度検知手段によって検知される検知温度が設定温度以上になった場合に前記熱交換器の伝熱管内にスケールが堆積していると判定する判定手段とを備え、
前記温度検知手段は、給湯運転時には常時燃焼する燃焼部の直上であって前記熱交換器の前記燃焼部に最も近い伝熱管の下流側の近傍において前記熱交換器缶体の表面に設けられたことを特徴とする給湯装置。 In a hot water supply apparatus comprising a fin-and-tube heat exchanger for heating clean water with combustion gas, and a heat exchanger can body for housing the heat exchanger,
A temperature detection means for detecting the surface temperature of the heat exchanger can body, and a scale accumulates in the heat transfer tube of the heat exchanger when the detected temperature detected by the temperature detection means exceeds a set temperature. Determination means for determining that the
The temperature detecting means is provided on the surface of the heat exchanger can body in the vicinity of the downstream side of the heat transfer tube closest to the combustion portion of the heat exchanger, immediately above the combustion portion that always burns during hot water supply operation. A water heater characterized by that.
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